ES2184783T3 - CATALYST REGENERATION PROCEDURE. - Google Patents

CATALYST REGENERATION PROCEDURE.

Info

Publication number
ES2184783T3
ES2184783T3 ES95306405T ES95306405T ES2184783T3 ES 2184783 T3 ES2184783 T3 ES 2184783T3 ES 95306405 T ES95306405 T ES 95306405T ES 95306405 T ES95306405 T ES 95306405T ES 2184783 T3 ES2184783 T3 ES 2184783T3
Authority
ES
Spain
Prior art keywords
nitrogen
combustion
coke
area
oxygen
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
ES95306405T
Other languages
Spanish (es)
Inventor
Raghu K Menon
Ramakrishnan Ramachandran
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Linde LLC
Original Assignee
BOC Group Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=23225462&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=ES2184783(T3) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by BOC Group Inc filed Critical BOC Group Inc
Application granted granted Critical
Publication of ES2184783T3 publication Critical patent/ES2184783T3/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
    • C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
    • C10G11/182—Regeneration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00—Catalysts comprising molecular sieves
    • B01J29/90—Regeneration or reactivation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/54—Nitrogen compounds
    • B01D53/56—Nitrogen oxides
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P30/00—Technologies relating to oil refining and petrochemical industry
    • Y02P30/40—Ethylene production

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • Materials Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Catalysts (AREA)
  • Industrial Gases (AREA)

Abstract

UN CATALIZADOR DE PIROLISIS DE HIDROCARBURO CON DEPOSITOS DE COQUE, SE REGENERA MEDIANTE LA COMBUSTION DE LOS DEPOSITOS EN UN REGENERADOR (2) CON UNA ZONA DE COMBUSTION INFERIOR (12) Y UNA ZONA REDUCTORA SUPERIOR (14). UNA MEZCLA DE OXIGENO Y UN GAS INERTE (POR EJEMPLO NITROGENO O DIOXIDO DE CARBONO) SE INTRODUCE EN LA ZONA DE COMBUSTION (12) A TRAVES DE UN DISTRIBUIDOR. LA ZONA DE COMBUSTION (12) TIENE AL MENOS UN 24% DE VOLUMEN DEL INDICE DE FLUJO TOTAL DE TODOS LOS GASES EN LA ZONA (12). SE COMBUSTIONA AL MENOS PARTE DEL COQUE. ADEMAS, EL NITROGENO EN EL COQUE SE CONVIERTE A OXIDOS DE NITROGENO (NO{SUB,X}). UN GAS DE COMBUSTION SUSTANCIALMENTE SIN OXIGENO, INCLUYE UN DIOXIDO DE CARBONO, OXIDOS DE NITROGENO Y AL MENOS UN 1% DE VOLUMEN DE MONOXIDO DE CARBONO, QUE FLUYE EN LA ZONA REDUCTORA (14) CON EL RESULTADO DE AL MENOS PARTE DE LOS OXIDOS DE NITROGENO REDUCIDOS A NITROGENO.A HYDROCARBON PIROLISIS CATALYST WITH COKE DEPOSITS WILL BE REGENATED BY COMBUSTION OF THE DEPOSITS IN A REGENERATOR (2) WITH A BOTTOM OF COMBUSTION AREA (12) AND A SUPERIOR REDUCING ZONE (14). A MIXTURE OF OXYGEN AND AN INERT GAS (FOR EXAMPLE NITROGEN OR CARBON DIOXIDE) IS INTRODUCED IN THE COMBUSTION AREA (12) THROUGH A DISTRIBUTOR. THE COMBUSTION AREA (12) HAS AT LEAST 24% VOLUME OF THE TOTAL FLOW RATE OF ALL GASES IN THE AREA (12). IT COMBUSTS AT LEAST PART OF THE COKE. IN ADDITION, THE NITROGEN IN THE COKE IS CONVERTED TO NITROGEN OXIDES (NO {SUB, X}). A COMBUSTION GAS SUBSTANTIELY WITHOUT OXYGEN, INCLUDES A CARBON DIOXIDE, NITROGEN OXIDES AND AT LEAST 1% OF CARBON MONOXIDE VOLUME, THAT FLOWS IN THE REDUCING ZONE (14) WITH THE RESULT OF AT LEAST ONE OR LESS THAN NITROGEN REDUCED TO NITROGEN.

ES95306405T 1994-09-30 1995-09-13 CATALYST REGENERATION PROCEDURE. Expired - Lifetime ES2184783T3 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US31565694A 1994-09-30 1994-09-30

Publications (1)

Publication Number Publication Date
ES2184783T3 true ES2184783T3 (en) 2003-04-16

Family

ID=23225462

Family Applications (1)

Application Number Title Priority Date Filing Date
ES95306405T Expired - Lifetime ES2184783T3 (en) 1994-09-30 1995-09-13 CATALYST REGENERATION PROCEDURE.

Country Status (16)

Country Link
US (1) US5908804A (en)
EP (1) EP0704516B1 (en)
JP (1) JP3913281B2 (en)
KR (1) KR100191974B1 (en)
CN (1) CN1098328C (en)
AU (1) AU688571B2 (en)
CA (1) CA2156464C (en)
DE (1) DE69529196T2 (en)
ES (1) ES2184783T3 (en)
MY (1) MY113199A (en)
NO (1) NO313793B1 (en)
NZ (1) NZ272844A (en)
PL (1) PL179607B1 (en)
TR (1) TR199501185A2 (en)
TW (1) TW350871B (en)
ZA (1) ZA957448B (en)

Families Citing this family (27)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1091650C (en) * 1999-11-30 2002-10-02 中国科学院兰州化学物理研究所 Catalyst for reducing nitrogen monoxide with carbon monoxide
US6991767B1 (en) * 2000-09-18 2006-01-31 Procedyne Corp. Fluidized bed gas distributor system for elevated temperature operation
US6491810B1 (en) 2000-11-01 2002-12-10 Warden W. Mayes, Jr. Method of producing synthesis gas from a regeneration of spent cracking catalyst
US6916417B2 (en) * 2000-11-01 2005-07-12 Warden W. Mayes, Jr. Catalytic cracking of a residuum feedstock to produce lower molecular weight gaseous products
US6913687B2 (en) * 2000-11-01 2005-07-05 Warden W. Mayes, Jr. Method of producing synthesis gas from a regeneration of spent cracking catalyst
US6579820B2 (en) 2001-03-21 2003-06-17 The Boc Group, Inc. Reactor modifications for NOx reduction from a fluid catalytic cracking regeneration vessel
US6505567B1 (en) * 2001-11-26 2003-01-14 Alstom (Switzerland) Ltd Oxygen fired circulating fluidized bed steam generator
ATE329985T1 (en) * 2002-03-27 2006-07-15 Shell Int Research METHOD FOR COMBUSTION OF COKE DURING REGENERATION OF AN FCC CATALYST.
US7026262B1 (en) * 2002-09-17 2006-04-11 Uop Llc Apparatus and process for regenerating catalyst
US20040074809A1 (en) * 2002-10-21 2004-04-22 George Yaluris Reduction of gas phase reduced nitrogen species in partial burn FCC processes
US20040262197A1 (en) * 2003-06-24 2004-12-30 Mcgregor Duane R. Reduction of NOx in low CO partial-burn operation using full burn regenerator additives
US20050100493A1 (en) * 2003-11-06 2005-05-12 George Yaluris Ferrierite compositions for reducing NOx emissions during fluid catalytic cracking
US20050100494A1 (en) 2003-11-06 2005-05-12 George Yaluris Ferrierite compositions for reducing NOx emissions during fluid catalytic cracking
MXPA06006133A (en) * 2003-12-05 2007-01-26 Intercat Inc Mixed metal oxide sorbents.
US7304011B2 (en) * 2004-04-15 2007-12-04 W.R. Grace & Co. -Conn. Compositions and processes for reducing NOx emissions during fluid catalytic cracking
US20050232839A1 (en) * 2004-04-15 2005-10-20 George Yaluris Compositions and processes for reducing NOx emissions during fluid catalytic cracking
ITBO20040296A1 (en) * 2004-05-11 2004-08-11 Itea Spa High efficiency and reduced environmental impact combustors, and processes for the production of electricity deriving from it
CA2606249C (en) 2005-04-27 2013-07-23 W.R. Grace & Co.-Conn. Compositions and processes for reducing nox emissions during fluid catalytic cracking
US7470412B2 (en) * 2005-12-21 2008-12-30 Praxair Technology, Inc. Reduction of CO and NOx in regenerator flue gas
KR100824763B1 (en) * 2006-09-25 2008-04-24 희성촉매 주식회사 A method for regenerating catalysts
US7954458B2 (en) * 2007-11-14 2011-06-07 Alstom Technology Ltd Boiler having an integrated oxygen producing device
US8618012B2 (en) 2010-04-09 2013-12-31 Kellogg Brown & Root Llc Systems and methods for regenerating a spent catalyst
US8618011B2 (en) 2010-04-09 2013-12-31 Kellogg Brown & Root Llc Systems and methods for regenerating a spent catalyst
CN102527208B (en) * 2010-12-30 2014-12-31 中国石油化工股份有限公司 Method for removing sulfur oxide and nitrogen oxide in catalytic cracking regenerated smoke
JP5660957B2 (en) * 2011-03-31 2015-01-28 独立行政法人石油天然ガス・金属鉱物資源機構 Regenerated hydrocracking catalyst and method for producing hydrocarbon oil
JP5660956B2 (en) 2011-03-31 2015-01-28 独立行政法人石油天然ガス・金属鉱物資源機構 Hydrocracking catalyst and method for producing hydrocarbon oil
US9890334B2 (en) 2015-06-09 2018-02-13 Exxonmobil Research And Engineering Company Fluid catalytic cracking unit with low emissions

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2985584A (en) * 1958-11-07 1961-05-23 Union Carbide Corp Regeneration of coked catalyst with controlled oxygen content of the regeneration gas
CA1152052A (en) * 1980-06-27 1983-08-16 William A. Blanton, Jr. Flue gas pollutants control in particulate catalyst regeneration
US4443551A (en) * 1982-01-11 1984-04-17 Texaco Inc. Method and new distributor for delivering high velocity gas from a gas distributor through a nozzle with decreased erosion in the nozzle
US4542114A (en) * 1982-08-03 1985-09-17 Air Products And Chemicals, Inc. Process for the recovery and recycle of effluent gas from the regeneration of particulate matter with oxygen and carbon dioxide
CA1242985A (en) * 1984-02-08 1988-10-11 William P. Hegarty Method for controlling fluidized catalytic cracker regenerator temperature and velocity with carbon dioxide
GB8428395D0 (en) * 1984-11-09 1984-12-19 Boc Group Plc Oxidation process
FR2580870B1 (en) * 1985-04-23 1987-09-25 Arnaud Jean APPARATUS FOR REGULATING CHARACTERISTICS OF A LIGHT BEAM, IN PARTICULAR OF A POWER LASER
EP0299650B1 (en) * 1987-07-09 1992-11-25 Mobil Oil Corporation Regeneration of fluid catalytic cracking catalysts
US4755282A (en) 1987-07-22 1988-07-05 Shell Oil Company Process for the reduction of NH3 in regeneration zone off gas by select recycle of certain-sized NH3 decomposition catalysts
US4744962A (en) 1987-07-22 1988-05-17 Shell Oil Company Process for the reduction of ammonia in regeneration zone off gas by select addition of NOx to the regeneration zone or to the regeneration zone off gas
AU614530B2 (en) * 1987-08-12 1991-09-05 Mobil Oil Corporation Nox control in fluidized bed combustion process
FR2624762B1 (en) * 1987-12-21 1990-06-08 Total France METHOD AND DEVICE FOR REGENERATING A FLUIDIZED BED CATALYST
US5021144A (en) 1989-02-28 1991-06-04 Shell Oil Company Process for the reduction of NOX in an FCC regeneration system by select control of CO oxidation promoter in the regeneration zone
US5268089A (en) 1992-06-24 1993-12-07 Mobil Oil Corporation FCC of nitrogen containing hydrocarbons and catalyst regeneration
US5308473A (en) * 1992-09-18 1994-05-03 Mobil Oil Corporation Low NOx FCC regeneration process and apparatus

Also Published As

Publication number Publication date
KR960010080A (en) 1996-04-20
JPH08173817A (en) 1996-07-09
AU3292795A (en) 1996-04-18
NO313793B1 (en) 2002-12-02
CA2156464C (en) 1999-07-20
KR100191974B1 (en) 1999-06-15
EP0704516B1 (en) 2002-12-18
TW350871B (en) 1999-01-21
NZ272844A (en) 1997-05-26
MY113199A (en) 2001-12-31
ZA957448B (en) 1996-04-17
AU688571B2 (en) 1998-03-12
TR199501185A2 (en) 1996-06-21
EP0704516A2 (en) 1996-04-03
DE69529196T2 (en) 2003-07-17
CN1098328C (en) 2003-01-08
DE69529196D1 (en) 2003-01-30
JP3913281B2 (en) 2007-05-09
NO953470L (en) 1996-04-01
CA2156464A1 (en) 1996-03-31
NO953470D0 (en) 1995-09-04
PL310693A1 (en) 1996-04-01
CN1126238A (en) 1996-07-10
EP0704516A3 (en) 1996-05-08
US5908804A (en) 1999-06-01
PL179607B1 (en) 2000-10-31

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